Heat and momentum transfer to a particle in a laminar boundary layer

2020 ◽  
Vol 889 ◽  
Author(s):  
Aaron M. Lattanzi ◽  
Xiaolong Yin ◽  
Christine M. Hrenya
Keyword(s):  
Boundary Layer ◽  
Momentum Transfer ◽  
Laminar Boundary Layer ◽  
Image Position ◽  
Heat And Momentum Transfer

Development of a laminar boundary layer under conditions of continuous incipient separation

1976 ◽  
Vol 76 (1) ◽  
pp. 55-66 ◽  
Author(s):  
N. Curle
Keyword(s):  
Boundary Layer ◽  
Pressure Distribution ◽  
Laminar Boundary Layer ◽  
Shape Parameter ◽  
Uniform Pressure ◽  
Continuous Change ◽  
Similar Series ◽  
Image Position ◽  
Incipient Separation

SynopsisThis paper, extending the work of Stratford [6] considers a boundary layer with uniform pressure when x < x0, and with the pressure in x > x0 so chosen that the layer is just on the point of separation for all x >x0. The required pressure distribution is shown to beThe displacement and momentum thicknesses are also derived as series in powers of ξ (and log ξ), and the shape parameter H then obtained as a similar series. The continuous change in H from the Blasius value (when ξ = 0) towards the Falkner-Skan [3] separation value is convincingly demonstrated, with the aid of the leading terms of an asymptomatic expansion for large ξ.

Heat and Momentum Transfer above Riblets in Turblent Boundary Layer

2004 ◽  
Vol 2004.41 (0) ◽  
pp. 83-84
Author(s):  
Yasushi TAKAHASHI ◽  
Kimio HASEGAWA ◽  
Kazumi TSUNODA
Keyword(s):  
Boundary Layer ◽  
Momentum Transfer ◽  
Heat And Momentum Transfer

On Similar Solutions of the Boundary Layer Equations for Air in Dissociation Equilibrium

1960 ◽  
Vol 64 (589) ◽  
pp. 36-37
Author(s):  
R. L. Dommett
Keyword(s):  
Boundary Layer ◽  
Flat Plate ◽  
Laminar Boundary Layer ◽  
Specific Heats ◽  
Boundary Layer Equations ◽  
Dissociation Equilibrium ◽  
Image Position ◽  
Similar Solutions

Using a Stewartson transformation defined byit is straightforward to show that in the two cases for which it is possible to find similar solutions to the laminar boundary layer equations withPr≠1,Le=1, that is stagnation flowsUe∝Xand flat plate flowsUe=constant, it is not necessary to assume anything about the specific heats to derive the equations given and solved by Beckwith.

Sign in / Sign up

Export Citation Format

Share Document